Preparation of crosslinked organic porous particlesrelated applications

ABSTRACT

Crosslinked organic polymeric porous particles have a crosslinked organic solid phase and discrete pores dispersed within the crosslinked solid phase which pores are isolated from each other. These porous particles are prepared using one or more water-in-oil emulsions containing a polyfunctional reactive compound, a reagent that causes crosslinking, optionally an ethylenically unsaturated polymerizable monomer, and optionally an organic solvent, and can include various marker materials.

RELATED APPLICATIONS

Reference is made to copending and commonly assigned U.S. Ser. No.13/______ filed on even date herewith by me and entitled CROSSLINKEDORGANIC POROUS PARTICLES (Attorney Docket K000020/JLT).

Reference is made to copending and commonly assigned U.S. Ser. No.13/______ filed on even date herewith by Nair and Jones and entitledARTICLE AND SYSTEM WITH CROSSLINKED ORGANIC POROUS PARTICLES (AttorneyDocket K000167/JLT).

Reference is made to copending and commonly assigned U.S. Ser. No.13/______ filed on even date herewith by Landry-Coltrain and Nair andentitled LASER-ENGRAVEABLE COMPOSITIONS AND FLEXOGRAPHIC PRINTINGPRECURSORS (Attorney Docket K000092/JLT).

Reference is made to copending and commonly assigned U.S. Ser. No.13/______ filed on even date herewith by Landry-Coltrain and Nair andentitled LASER-ENGRAVEABLE COMPOSITIONS AND FLEXOGRAPHIC PRINTINGPRECURSORS (Attorney Docket K000093/JLT).

FIELD OF THE INVENTION

This invention relates to a method for preparing crosslinked organicporous particles having at least two discrete pores within a solidcrosslinked organic polymer phase. The method includes the formation ofan oil-in-water-in-oil emulsion. The crosslinked organic porousparticles can be used in various articles including imaging elements.

BACKGROUND OF THE INVENTION

Porous polymeric particles have been prepared and used for manydifferent purposes. For example, porous particles have been describedfor use in chromatographic columns, ion exchange and adsorption resins,drug delivery devices, cosmetic formulations, papers, and paints. Themethods for generating pores in polymeric particles are well known inthe field of polymer science. However, each particular porous particleoften requires unique methods for their manufacture. Some methods ofmanufacture produce large particles without any control of the pore sizewhile other manufacturing methods control the pore size withoutcontrolling the overall particle size and particle size distribution.

U.S. Pat. No. 3,957,741 (Rembaum et al.) describes crosslinked acrylateporous polymer particles having an average size less than 2 μm andvarious functional groups incorporated in the polymer.

U.S. Pat. No. 4,775,699 (Cozens) describes skinless porous polyvinylchloride (PVC) particles having greater than 20% of the surface areamade up of PVC and a particle size greater than 70 μm.

U.S. Pat. No. 6,780,942 (Leon et al.) describes porous particlesprepared from various polyesters, which particles have pores in theouter surfaces.

In the publication by C. M. Cheng, J. W. Vanderhoff, and M. S.El-Aasser, J. Polym. Sci.: Part A, Polymer Chemistry, Vol. 30, pp.245-256, 1992, the authors described porous particles having a pore sizeless than 100 nm and a particle size of 10 μm that are swellable inorganic solvents.

Marker material can be included in porous particles so that theparticles can be detected for a specific purpose. For example, U.S.Patent Application Publications 2008/0176157 (Nair et al.) and2010/0021838 (Putnam et al.) and U.S. Pat. No. 7,754,409 (Nair et al.)describe porous particles and a method for their manufacture, whichporous particles are designed to be toner particles for use inelectrophotography. Such porous particles typically contain a colorantsuch as carbon black or another pigment to provide desiredblack-and-white or color electrophotographic images. Such porousparticles (“toners”) can be prepared using a multiple emulsion processin combination with a suspension process (such as “evaporative limitedcoalescence”, ELC) in a reproducible manner and with a narrow particlesize distribution.

Still another important use of polymeric particles is as a means formarking documents, clothing, or labels as a “security” tag. For example,U.S. Pat. No. 5,385,803 (Duff et al.) describes a process ofauthentication of documents using an electrophotographic process andcore-shell toner particles containing an infrared emitting component anda detection step. U.S. Patent Application Publication 2003/0002029(Dukler et al.) describes a method for labeling documents forauthentication using a toner particle containing two or more mixedcompounds having a characteristic detectable signal.

Product counterfeiting occurs in artworks, CD's, DVD's, computersoftware recorded on various media, perfumes, designer clothes,handbags, luggage, automobile and airplane parts, securities (forexample stock certificates), identification cards (for example, drivers'licenses, passports, visas, and green cards), credit and debit cards,smart cards, and pharmaceuticals. The application of a security markeror taggant to an object or product for authenticating the origin orintended market is known in the art. Security markers can beincorporated into components that make up the object or product, or theycan be incorporated into papers, inks, or varnishes that are applied tothe object or product, or they can be incorporated into labels affixedto the object, product, or packaging there for. The presence of thesecurity marker can be used to verify the authenticity of the origin ofthe object using suitable detection means that is specific to thesecurity marker.

Some systems used for detecting the security markers are often known as“forensic” systems because they tend to require sophisticated equipment(for example high power microscopes) in a laboratory analysis. Otherdetection systems are designed for “field” use and are known as “covert”systems as they can be used outside the laboratory with speciallydesigned equipment for the specific security markers being detected.

Some security markers can be dispersed within a carrier varnish and arereferred to as particle-based or pigment-based markers. Such markersremain intact in the varnish and will appear as particles when examinedmicroscopically. Other security markers are dissolvable in an ink orvarnish and distributed in the carrier on a molecular level. Thesemarkers are not readily detected with a microscope and require moresophisticated detection equipment.

A means for detecting a population of microparticles is described inU.S. Pat. No. 5,450,190 (Schwartz et al.). Groups of microparticles ofspecific sizes and fluorescent properties or colors are mixed with tonerparticles and the resulting mixture is used in laser printer cartridgesor photocopy machines to provide detectable images.

Particles having two or more different light emitting species can alsobe printed onto various substrates using various printing means, asdescribed in WO 2007/051035 (Haushalter).

Toner particles having a luminescent material that includes quantum dotsare described in EP 2,025,525 (Wosnick et al.) and can be used to formdetectable markings on substrates. These toner particles can alsoinclude colorants or other detectable components.

Copending and commonly assigned U.S. Ser. No. 12/984,030 that was filedby Nair, Jennings, Jones, and Sedita, Ser. No. 12/984,044 that was filedby Nair, Jones, and Kapp, and Ser. No. 12/984,055 that was filed byNair, Jennings, Jones, Sedita, and Olm, all on Jan. 4, 2011, describeporous particles that contain two or more different markers in discretepores and various uses and methods of preparation. Such porous particleshave various utilities including authentication, security(anti-counterfeiting), and electrophotographic purposes as describedabove.

While the noted porous particles represent an important advance in theart, there is a desire for improved porous particles that have increasedresistance to organic solvents, high temperatures, and pressure.

SUMMARY OF THE INVENTION

The present invention provides a method for preparing a crosslinkedorganic porous particle comprising: providing a first water-in-oilemulsion comprising a first pore stabilizing hydrocolloid in a firstaqueous phase that is dispersed in a first oil phase, which first oilphase comprises a first polyfunctional reactive compound, a firstreagent that causes crosslinking, optionally at least one firstethylenically unsaturated polymerizable monomer, and optionally a firstorganic solvent, and

optionally providing a second water-in-oil emulsion comprising a secondpore stabilizing hydrocolloid in a second aqueous phase that isdispersed in a second oil phase, which second oil phase comprises asecond polyfunctional reactive compound, a second reagent that causescrosslinking, optionally at least one ethylenically unsaturatedpolymerizable monomer, and optionally a second organic solvent,

optionally combining the first and second water-in-oil emulsions to forma third water-in-oil emulsion containing a mixture of the first andsecond oil phases and distinct droplets of the first and second aqueousphases,

dispersing either the first water-in-oil emulsion or the thirdwater-in-oil emulsion in a third aqueous phase containing a surfacestabilizing agent to form a water-in-oil-in-water emulsion containingdroplets of either the first water-in-oil emulsion or droplets of thethird water-in-oil emulsion, which third water-in-oil emulsion dropletscontain the distinct droplets of the first and second aqueous phases,and

polymerizing the polyfunctional reactive compounds and optionally theethylenically unsaturated polymerizable monomers to form a precursorcrosslinked organic porous particle having a crosslinked organic solidphase including an external particle surface, and discrete pores,optionally first and second discrete pores, being isolated from eachother and dispersed within the crosslinked organic solid phase,

removing, if present, the first and second organic solvents to producean aqueous suspension of the precursor crosslinked organic porousparticle, and

isolating the precursor crosslinked organic porous particle to provide acrosslinked organic porous particle.

This method can further comprise:

combining one or more additional water-in-oil emulsions (beyond thefirst and second water-in-oil emulsions), each comprising a porestabilizing hydrocolloid in one or more additional aqueous phases thatare dispersed in one or more additional oil phases each, and each oilphase containing a polyfunctional reactive compound, a reagent thatcauses crosslinking, optionally an ethylenically unsaturatedpolymerizable monomer, and optionally an organic solvent,

with the first and second water-in-oil emulsions so that the thirdwater-in-oil emulsion contains distinct droplets of the first, second,and the one or more additional aqueous phases.

If there are two or more marker materials in discrete pores, thesedetectably different marker materials are isolated from each other indifferent sets of discrete pores to provide a unique signature that isdifferent from a signature that is obtained by mere mixing of the markermaterials in the same domain (for example, in the same pores). Suchcrosslinked organic porous particles can be used in unique applicationswhere different marker materials are needed for detection,authentication, or other purposes. Alternatively, mixtures of multipletypes of crosslinked organic porous particles can be designed in whicheach type of crosslinked organic porous particle can have two or moredetectably different marker materials that can additionally bemanipulated by desired stimuli if desired.

The present invention provides a number of advantages. For example, itprovides crosslinked organic porous particles that can be designed tohave one or more detectably different marker materials within the samecrosslinked organic porous particle. There is no need to have markermaterials or reagents on the external particle surface. Nor is there aneed to have open pores on the external particle surface for diffusionof materials into and out of the crosslinked organic porous particles.

Because the organic porous particles are crosslinked in the solidorganic polymeric phase, they are much more resistant to hightemperatures, pressures, various organic solvents and monomers that canbe present in lacquers, varnishes, coating solvents, and melt processingtemperature used to prepare imaging elements such as flexographicprinting precursors. This crosslinked property increases the number ofuses for the organic porous particles compared to non-crosslinkedorganic porous particles. In addition, the crosslinked organic porousparticles have limited swellability in organic solvents such as propylacetate as described below.

Such crosslinked organic porous particles can be prepared using uniquemethods using multiple water-in-oil emulsions. The crosslinked organicporous polymer particle size, size distribution, pore sizes, and typesof marker materials can be controlled by the amount and type of“porogen” used to create the pores, the fraction of the first or secondwater phase relative to the oil phase, the relative quantity and type ofpolyfunctional reactive compound used, the relative quantity and type ofsolvents, the type and amounts of stabilizers and emulsifiers, and thetype of shear that is used in dispersing one or more phases into thecrosslinked polymer solid phase, and the amount of water-in-oil emulsionin the third water phase used to form the multiple emulsion. It is alsopossible to make crosslinked organic porous particles that are eitherspherical or less than spherical for various advantages.

In the method of preparing the crosslinked organic porous particles, oneor more polyfunctional reactive compounds that can act as crosslinkingagents are used to prepare the crosslinked solid polymer phase.Polyfunctional reactive compounds can be polyunsaturated compoundsincluding both prepolymers and monomers capable of chain growthpolymerization with reagents that cause crosslinking such as azocompounds or peroxides that are free radical initiators, and can also bereactive polymers such as those with carboxylic acid groups that arecapable of step growth reactions with reagents that cause crosslinkingsuch as polyfunctional aziridines or polyfunctional glycidyl compounds.

DETAILED DESCRIPTION OF THE INVENTION

As noted above, the crosslinked organic porous particles prepared usingthis invention can have various uses including but not limited to usein, chromatographic columns, ion exchange and adsorption resins, drugdelivery devices, cosmetic formulations, pharmaceuticals, papers,fabrics, fibers, paints, inks, adhesives, electrophotographic toners,and security systems for detection of counterfeits, documentauthentication, and labeling of consumer goods (such as designerclothes, handbags, perfumes, and cosmetics). They can also be used inpaper and plastic cards, for example driver's licenses, passports, andother identification cards. Moreover, the crosslinked organic porousparticles can be incorporated into packaging and packaging componentssuch as labels, tape, staples, foils, plastics, paperboard, andcardboard packing The crosslinked organic porous particles can also beincluded in varnishes (colored or colorless) and other coatingcompositions, polymeric films and fibers, and formed polymer, glass, andceramic articles including ceramic substrates, bottles, and bottle caps.In some embodiments, the crosslinked organic porous particles can bemelt-compounded or otherwise incorporated into a plastic and become anintegral part of a packaging material.

The crosslinked organic porous particles also can be used inlaser-engraveable flexographic relief-forming layers to enhance laserablation rates in flexographic printing precursors. Such precursors aredescribed in copending and commonly assigned U.S. Ser. Nos. 13/______and 13/______ both filed on even date herewith by Landry-Coltrain andNair, as noted above (Attorney Dockets K000092/JLT & K000093/JLT).

The crosslinked organic porous particles are generally prepared, asdescribed below, using multiple water-in-oil emulsions in combinationwith an aqueous suspension process, such as in the ELC process. One ormore water-in-oil emulsions can be originally prepared and used toprovide two or more discrete pores in the crosslinked organic porousparticles.

The terms “crosslinked organic porous particle” and “crosslinked organicporous particles” are used herein, unless otherwise indicated, to referto materials prepared according to the present invention. Thecrosslinked organic porous particles comprise a crosslinked solid(organic polymer) phase having an external particle surface and discretepores (an least first and second different discrete types of pores asdefined below) dispersed within the crosslinked organic solid phase andone or more marker materials, such as first and second marker materialsthat are exclusively within the first and second discrete pores,respectively.

The term “crosslinked” refers to the instance when the components of acomposition or material are linked together by chemical bonds that linkone polymer chain to another and involve joining together two or morepolymeric molecules with bonds that are strong. These bonds can becovalent or ionic in nature although irreversible covalent bonds arebest.

In many embodiments, the crosslinked organic solid phase of thecrosslinked organic porous particles has the same composition. That is,the crosslinked organic solid phase is uniform in composition includingany additives that are distributed within the crosslinked polymerbinder. In addition, if mixtures of organic polymers are present in thecrosslinked organic solid phase, those organic polymeric mixtures aredispersed uniformly throughout the porous particles.

Unless otherwise indicated herein, when used to define variouscomponents, chemicals, or materials, the articles “a”, “an”, and “the”refer to one or more (plurality) of those components, chemicals, ormaterials.

The terms “detectably different” or “detectably distinct” refer todifferent marker materials (or different mixtures of marker materialsdescribed below) being detectable from each other using suitabledetection means.

The term “porogen” refers to a pore forming agent used to make thecrosslinked organic porous particles. In this invention, a porogen canbe the aqueous phase of the water-in-oil emulsions (that is the firstand second aqueous phases), the pore stabilizing hydrocolloid, and anyother additive in the aqueous phase that can modulate the porosity ofthe crosslinked organic porous particles.

As used in this disclosure, the term “isolated from each other” refersto the first and second marker materials being in different (distinct)pores. In other words, the first marker material is only in certain(first) pores and the second marker material is present only indifferent (second) pores. Each of these sets of pores can include othermarker materials or materials that do not behave as marker materials aslong as the first and second marker materials are purposely not locatedwithin the same pores. Another way of defining this feature is that thefirst marker materials are in the first discrete pores exclusively andthe second marker materials are in the second discrete poresexclusively.

The terms “first discrete pore” and “second discrete pore” refer todifferent isolated pores in the porous particle that can containdifferent marker materials. First and second discrete pores can refer todistinct individual pores, or in most embodiments, they refer todistinct sets of pores. Each set of pores includes a plurality of pores,which pores are isolated from each other, and the pores of each set ofpores are isolated from all other pores of the other sets of pores inthe crosslinked organic porous particle. The first discrete pores can beempty or comprise a first marker material and the second discrete porescan contain a second marker material, and any additional discrete pores(beyond the first and second discrete pores) can optionally containstill a different marker material. The word “discrete” is also used todefine different droplets of the first and second aqueous phases whenthey are suspended in the oil phase (described below).

The size of the crosslinked organic porous particle, the formulation,and manufacturing conditions are the primary controlling factors forpore size. However, generally the discrete pores have an average size ofat least 100 nm (0.1 μm) and up to and including 4000 nm (4 μm), or morelikely at least 100 nm (0.1 μm) and up to and including 2000 nm (2 μm).The discrete pores in the crosslinked organic porous particles (forexample, the first and second discrete pores) can have the same ordifferent average sizes. Pore size can be determined by analyzingScanning Electron Microscopy (SEM) images of fractured crosslinkedorganic porous particles using a commercial statistical analysissoftware package to study the distribution of the pores within thecrosslinked organic porous particles, or by manually measuring the porediameters using the scale in the SEM images. For example, the “average”pore size can be determined by calculating the average diameter of 20measured pores.

The crosslinked organic porous particles generally have a mode particlesize of at least 3 μm and up to and including 100 μm, or typically atleast 5 μm and up to and including 70 μm, or up to and including 50 μm,with this mode particle size being measured by, for example, automatedimage analysis and flow cytometry using any suitable equipment designedfor this purpose. The mode particle size represents the most frequentlyoccurring diameter for spherical crosslinked organic porous particlesand the most frequently occurring largest diameter for the non-sphericalporous particles in a particle size distribution histogram.

The crosslinked organic porous particles of this invention can also havesmall colloidal inorganic particles on the external particle surfaces.These colloidal inorganic particles can be interspersed on the externalparticle surfaces or they can be arranged in a pattern or entirely coverthe external particle surfaces in a layer. Such colloidal inorganicparticles can be composed of, for example, colloidal silica, colloidalalumina, colloidal titania, clay particles, or mixtures thereof. Thesecolloidal inorganic particles can be individual particles, or aggregatesof particles, ranging in particle or aggregate size of at least 5 nm andup to and including 2 μm.

In general, the crosslinked organic porous particles have porosity of atleast 1% and up to and including 80%, or more likely at least 1% and upto and including 50%, or typically at least 10% and up to an including30% to improve visualization of the marker particles in the crosslinkedorganic porous particles, all based on the total crosslinked organicporous particle volume. Porosity can be measured by the mercuryintrusion technique or a time-of-flight method.

The discrete pores (such as first and second discrete pores) can alsocomprise pore stabilizing hydrocolloids that are described below. Ifboth the first and second discrete pores are present, they can have thesame or different stabilizing hydrocolloids. In most instances, the samepore stabilizing hydrocolloid is used throughout the crosslinked organicporous particles.

The crosslinked organic porous particles can be spherical ornon-spherical depending upon the desired use. Non-spherical crosslinkedorganic porous particles can be advantageous for improved detection ofthe marker materials. The shape of crosslinked organic porous particlescan be characterized by an “aspect ratio” (AR) that is defined as theratio of the largest perpendicular length to the longest length of theparticle. These lengths can be determined for example by opticalmeasurements using a commercial particle shape analyzer such as theSysmex FPIA-3000 (Malvern Instruments). For example, crosslinked organicporous particles that are considered “spherical” for this invention canhave an aspect ratio of at least 0.9 and up to and including 1. For thenon-spherical crosslinked organic porous particles of this invention,the aspect ratio can be as low as 0.1 and up to and including 0.95, andin some embodiments, the aspect ratio can be less than 0.95 and down toand including 0.4.

As described above, the crosslinked organic porous particles can includetwo or more marker materials that are detectably different. Forconvenience, when two detectably different marker materials are includedwithin a crosslinked organic porous particle, they are labeled “first”and “second” marker materials to distinguish them. If additionaldetectably different marker materials are present in the same ordifferent crosslinked organic porous particles, they are labeled,“third”, “fourth”, “fifth”, and so forth, marker materials.

As defined herein, the first marker material can be present in a firstdiscrete pore, a second marker material can be present in a seconddiscrete pore, and additional marker materials (besides the first andsecond marker materials) can be present in additional discrete pores(besides the first and second discrete pores) of the crosslinked organicporous particle. These additional discrete pores can have an additionaldetectably different marker material.

In some embodiments, either the first or second discrete pores contain amarker material but the other set of discrete pores are “empty” (nomarker material).

In some other embodiments, the crosslinked organic porous particles canhave three or four additional discrete pores and each of these sets ofdiscrete pores has a detectably different marker material wherein atleast two of the detectably different marker materials in the three orfour additional sets of discrete pores are detectably different fromeach other. Each of these markers in the three or four additionaldiscrete pores is generally detectably different from all of the othermarker materials in the crosslinked organic porous particle (that is,different from the first and second marker materials).

In still other embodiments, the crosslinked organic porous particles canhave three or four additional discrete pores (beyond the first andsecond discrete pores) and they can have at least one more markermaterial than there are discrete sets of pores, so that at least one setof discrete pore has two or more (multiple) marker materials.

The detectably different marker materials can be different colored dyesor pigments (or colorants), or metallic pigments, that are generally notwater soluble. Such colorants can include but are not limited to, thosedescribed in U.S. Reissue Pat. No. 31,072 (Jadwin et al.) and in U.S.Pat. No. 4,160,644 (Ryan), and U.S. Pat. No. 4,416,965 (Sandhu et al.),U.S. Pat. No. 4,414,152 (Santilli et al.), such as carbon black, AnilineBlue, Calcoil Blue, Chrome Yellow, Ultramarine Blue, Du Pont Oil Red,Quinoline Yellow, Methylene Blue Chloride, Phthalocyanine Blue,Malachite Green Oxalate, Lamp Black, Rose Bengal, C.I. Pigment Red 48:1,C.I. Pigment Red 122, C.I. Pigment Red 57:1, C.I. Pigment Yellow 97,C.I. Pigment Yellow 12, C.I. Pigment Yellow 17, C.I. Pigment Blue 15:1,and C.I. Pigment Blue 15:3. Other useful colorants are described in U.S.Pat. No. 5,385,803 (Duff et al.) and EP 2,025,525 (Wosnick et al.) thatare incorporated herein by reference. The marker materials can vary inwater solubility although most have little water-solubility. Each markermaterial can include mixtures of colorants as long as the mixtures ofmarker materials in the crosslinked organic porous particle aredetectably different. Thus, the first and second marker materials can bemixtures of marker materials as long as the mixtures are detectablydifferent.

Other classes of marker materials useful in the practice of thisinvention include but are not limited to, different fluorescingmaterials, radioisotopes, particles of metals and metal-containingcompounds (such as metal oxides, metal sulfides, and metaloxyhydroxides) having different magnetic moments, luminescing compounds,as well as bioactive materials. Certain reactive chemicals can be usedas markers and kept separate in discrete pores until their reaction isneeded. Examples of such reactive chemicals include acids and bases, andisocyanates and amines.

Examples of useful fluorescing marker materials include but are notlimited to, compounds that absorb radiation (excite) in the UV andvisible regions of the electromagnetic spectrum but then emit orfluoresce in the infrared or visible region of the electromagneticspectrum. Other useful fluorescing marker materials absorb radiation(excite) in the infrared region and also fluoresce in the infraredregion. Still other fluorescing marker materials absorb (excite) in theinfrared region and fluoresce in the visible region. Fluorescent lightactivated dyes can be invisible to or exhibit one color under ambientlight conditions and a second color under fluorescent light conditions.Fluorescent dyes are known to the person skilled in the art. Examples ofsuch compound include but are not limited to, coumarins, perylenes,naphthalimides, cyanines including metal phthalocyanines and metalnaphthocyanines, xanthenes, oxazines, anthracene, naphthacene,anthraquinone, and thiazine dyes and derivatives thereof so as to makethem water-soluble or water-dispersible.

Examples of useful emissive inorganic marker materials include but arenot limited to, CaWO₄:Eu; CaMoO₄:Mn,Eu; BaFBr:Eu; Y₂O₂S:Tb; Y₂O₂S:Er,Yb;Y₂O₂S:Er; Y₂O₂S:Eu; Y₂O₃:Eu; Y₂O₃S:Eu+Fe₂O₃; Gd₂O₂S:Tb; Gd₂O₂S:Eu;Gd₂O₂S:Nd; Gd₂O₂S:Yb,Nd; Gd₂O₂S:Yb,Tm; Gd₂O₂S:Yb,Tb; Gd₂O₂S:Yb,Eu;LaOF:Eu; La₂O₂S:Eu; La₂O₂S:Eu,Tb; La₂O₂S:Tb; BaMgAl₁₆O₂₇:Eu;Y₂SiO₅:Tb,Ce; Y₃Al₅O₁₂:Ce; Y₃Al_(2.5)Ga_(2.5)O₁₂:Ce; YVO₄:Nd; YVO₄:Eu;Sr₅(PO₄)₃Cl:Eu; CaS:Eu; ZnS:Ag; ZnSiO₄:Mn; CaSiO₃:Mn; ZnS:Bi;(Ca,Sr)S:Bi; (Zn,Mg)F₂:Mn; CaWO₄; CaMoO₄; ZnO:Zn; ZnO:Bi; TiO₂, andKMgF₃:Mn.

Visible light emitting compounds that are excited by exposure to UVradiation can be used including rare earth emitting compounds that aredescribed in numerous publications including WO2007/051035 (Haushalter)that is incorporated herein by reference.

Examples of useful radioisotope marker materials include but are notlimited to ³²P, ³H, ¹⁴C, ⁴¹Ca, ⁵⁷Co and ⁵⁹Fe.

Examples of useful metal and metal-containing marker materials withdifferent magnetic moments include but are not limited to, particles ofiron, nickel, cobalt, and gadolinium, as well as particles of metaloxides, metal sulfides, metal oxysulfides, and metal oxyhydroxides.Other metal-containing compounds that would be useful as markermaterials would be readily apparent to a skilled artisan. While manymetal marker materials are insoluble in water or organic solvents, othermetal marker materials are colloidal or suspendible materials in wateror organic solvents.

It is particularly useful in some embodiments that the crosslinkedorganic porous particles comprise a radiation absorber in one or more ofthe sets of discrete pores, and particularly useful radiation absorbersare infrared radiation absorbers or ultraviolet radiation absorbers.Such embodiments can be useful in flexographic laser-ablatable layersthat can be used in flexographic printing precursors, or other reliefimage-forming elements.

Examples of infrared (IR) radiation absorbers include compounds thatemit infrared radiation having a wavelength of at least 700 nm and up toand including 1500 nm when irradiated with light having a shorterwavelength. Such compounds include but are not limited to, metalphthalocyanines, vanadyl phthalocyanines, copper phthalocyanines, metalfree phthalocyanines, azines dyes, chlorophylls, and laser dyes. Variouscarbon blacks (conductive or non-conductive carbon blacks) are alsouseful as IR absorbers.

Luminescing compounds that have the capability of being illuminated uponexposure to activating radiation include those described in EP 2,025,525(noted above).

Examples of chemicals that can be used as marker materials and can thenreact when mixed include but are not limited to, isocyanates, amines,epoxies, carboxylic acids, hydroxyl compounds, silanes, silica, aluminaand other such sols.

The various marker materials (such as the first and second markermaterials) can be present, independently, in an amount of at least 0.001weight % and up to and including 35 weight %, or at least 0.001 weight %and up to and including 25 weight %, all based on total crosslinkedorganic porous particle weight. A skilled worker would understand thatthe various types of marker materials can be present in differentamounts, depending for example on the amounts needed for detectabilityor the relative amounts of the marker materials needed in a specificcrosslinked organic porous particle.

In some embodiments, the amount of the first marker material in relationto the amount of the second marker material is at a 1:2 to 2:1 weightratio.

If the crosslinked organic porous particles are to be used as tonerparticles in electrophotographic processes, the crosslinked organicporous particles can also include one or more release agents such aswaxes and lubricants. Examples of useful release agents are provided forexample in U.S. Patent Application Publication 2008/0176157 (Nair etal.) that is incorporated herein by reference. Such compounds can bepresent in an amount of at least 0.1 weight % and up to and including 20weight % based on the crosslinked organic porous particle dry weight.

In addition, such crosslinked organic porous toner particles can alsoinclude one or more charge control agents (either negative or positivecharge control agents). Examples of such compounds are also described inU.S. Patent Application Publication 2008/0176157 (noted above). They canbe present in an amount of at least 0.1 weight % and up to and including5 weight %, based on the crosslinked organic porous particle dry weight.

While in many embodiments, all of the pores in the crosslinked organicporous particles contain one or more marker materials, the crosslinkedorganic porous particles can also include additional discrete poresbesides the first and second discrete pores, and some of theseadditional discrete pores can have a marker material different from thefirst and second marker materials. Alternatively, some of theseadditional discrete pores have no marker material (they are void or“empty” of marker materials). Additionally, in yet other embodiments,all of the pores have no marker material, or all contain the same markermaterial.

While the pores can be completely filled with the individual markermaterials, it is also possible that only parts of the pores are filledwith the marker materials. For example, marker materials can be disposedon the inner wall of the respective first or second discrete pores,thereby leaving a void (unoccupied volume) within the interior of thefirst and second discrete pores, respectively.

In the embodiments comprising mixtures of different crosslinked organicporous particles (for example, a mixture of first and second crosslinkedorganic porous particles) in which the crosslinked organic solid phaseshave the same or different polymer compositions.

In addition, the mixture of first and second crosslinked organic porousparticles can include first, second, third, and fourth marker materialsthat are all different, or only three of the marker materials aredifferent and two of the marker materials can be the same. Some discretepores can contain multiple (two or more) marker materials.

In still other embodiments, the first and third marker materials are thesame, and the second and fourth marker materials are different from allother marker materials.

The crosslinked organic porous particles or mixtures of differentcrosslinked organic porous particles can be provided as powders, or asaqueous suspensions (including water or water with water-miscibleorganic solvents such as alcohols). Such aqueous suspensions can alsoinclude surfactants or suspending agents to keep the crosslinked organicporous particles suspended. In addition, the crosslinked organic porousparticles can be provided in organic solvent suspensions using forexample, in one or more of methanol, ethanol, isopropanol, acetone,ethyl acetate, propyl acetate, cyclohexane, dodecane, and toluene asorganic solvents or in organic varnishes or lacquers.

The other compositional features are described in the followingdescription of methods for preparing the crosslinked organic porousparticles. The polyfunctional reactive compounds, reagents that causecrosslinking, ethylenically unsaturated polymerizable monomers, organicsolvents, and pore stabilizing hydrocolloids used to form thecrosslinked organic polymer solid phase of the crosslinked organicporous particles are described below.

Methods of Preparing Crosslinked Organic Porous Particles

A method for making the crosslinked organic porous particles involvesthe formation of one or more (for example, first and second)water-in-oil emulsions. A first stable water-in-oil emulsion is formed,including a first aqueous phase that is dispersed in a first oil phase.This first oil phase comprises a first polyfunctional reactive compound,a first reagent that causes crosslinking, optionally at least one firstethylenically unsaturated polymerizable monomer, and optionally a firstorganic solvent. The first aqueous phase creates the first discretepores in the resulting crosslinked organic porous particles. The firstaqueous phase can also include a first pore stabilizing hydrocolloid anda first marker material. Thus, the first water-in-oil emulsion cancomprise a first marker material that is eventually incorporated intothe first discrete pores.

Useful polyfunctional reactive compounds, reagents that causecrosslinking, ethylenically unsaturated polymerizable monomers, andorganic solvents are described below. They are used to form acrosslinked organic solid phase (polymer phase) in the crosslinkedorganic porous particles.

The method can optionally provide a second water-in-oil emulsioncomprising a second aqueous phase comprising a second pore stabilizinghydrocolloid (and optionally, a second marker material) dispersed in asuitable second oil phase. This second oil phase comprises a secondpolyfunctional reactive compound, a second reagent that causescrosslinking, optionally at least one second ethylenically unsaturatedpolymerizable monomer, and optionally a second polymerization initiator,and optionally a second organic solvent. This second aqueous phasecreates the second discrete pores in the resulting crosslinked organicporous particles. As described above, the second marker material isdetectably different from the first marker material. Thus, the secondwater-in-oil emulsion can comprise a first second marker material thatis eventually incorporated into the second discrete pores.

The first and second pore stabilizing hydrocolloids (described below)can be the same or different chemicals, or the same or differentmixtures of chemicals. In most embodiments, they are the same chemicals.In addition, the first and second oil phases can comprise the same ordifferent organic solvents (described below), or the same or differentmixtures of organic solvents. In most embodiments, the first and secondoil phases contain the same organic solvents. Further, the first andsecond polyfunctional reactive compounds or first and secondethylenically unsaturated monomers and first and second reagents thatcause crosslinking used in preparing the first and second oil phases canbe the same or different compounds, or mixtures of compounds, but inmost embodiments, they are the same compounds in both oil phases.

Suitable pore stabilizing hydrocolloids for preparing all of theemulsions described herein include both naturally occurring andsynthetic, water-soluble or water-swellable polymers selected from thegroup consisting of cellulose derivatives [such for example,carboxymethyl cellulose (CMC) that is also referred to as sodiumcarboxymethyl cellulose], gelatin (for example, alkali-treated gelatinsuch as cattle bone or hide gelatin, or acid treated gelatin such aspigskin gelatin), gelatin derivatives (for example, acetylated gelatinand phthalated gelatin), proteins and protein derivatives, hydrophilicsynthetic polymers [such as poly(vinyl alcohol), poly(vinyl lactams),acrylamide polymers, polyvinyl acetals, polymers of alkyl and sulfoalkylacrylates and methacrylates, hydrolyzed polyvinyl acetates, polyamides,polyvinyl pyridine, and methacrylamide copolymers], water solublemicrogels, polyelectrolytes [such as a polystyrene sulfonate,poly(2-acrylamido-2-methylpropanesulfonate), and a polyphosphate], andmixtures of any of these classes of materials.

In order to stabilize the initial water-in-oil emulsions so that theycan be held without ripening or coalescence, it is desired that the porestabilizing hydrocolloids in the aqueous phase have a higher osmoticpressure than that of the first and second oil phases depending on thesolubility of water in the oil. This reduces the diffusion of water intothe oil phases from the aqueous phases and thus the ripening caused bymigration of water between the water droplets. One can achieve a higherosmotic pressure in the aqueous phase either by increasing theconcentration of the pore stabilizing hydrocolloid or by increasing thecharge on the pore stabilizing hydrocolloid (the counter-ions of thedissociated charges on the pore stabilizing hydrocolloid increase itsosmotic pressure). It can be advantageous to have weak base or weak acidmoieties in the pore stabilizing hydrocolloids that allow for theirosmotic pressures to be controlled by changing the pH. Such porestabilizing hydrocolloids are considered “weakly dissociatinghydrocolloids”. For these weakly dissociating hydrocolloids, the osmoticpressure can be increased by buffering the pH to favor dissociation, orby simply adding a base (or acid) to change the pH of the aqueous phaseto favor dissociation. One example of such a weakly dissociatinghydrocolloid is CMC that has a pH sensitive dissociation (thecarboxylate is a weak acid moiety). For CMC, the osmotic pressure can beincreased by buffering the pH, for example using a pH 6-8 buffer, or bysimply adding a base to raise the pH of the aqueous phase to favordissociation. For aqueous phases containing CMC the osmotic pressureincreases rapidly as the pH is increased from 4-8.

Other synthetic polyelectrolyte hydrocolloids such as polystyrenesulfonate (PSS), poly(2-acrylamido-2-methylpropanesulfonate) (PAMS), andpolyphosphates are also useful pore stabilizing hydrocolloids.

For example, the first and second pore stabilizing hydrocolloids are thesame or different and independently selected from the group consistingof carboxymethyl cellulose (CMC), a gelatin, a protein or proteinderivative, a hydrophilic synthetic polymer, a water-soluble microgel, apolystyrene sulfonate, poly(2-acrylamido-2-methylpropanesulfonate), apolyphosphate, and mixtures thereof.

The pore stabilizing hydrocolloids are soluble in water, have nonegative impact on multiple emulsification processes, and have nonegative impact on melt rheology of the resulting crosslinked organicporous particles that, for example, can be used as electrophotographictoners. The pore stabilizing compounds can be optionally crosslinked tominimize migration of these compounds to the particle outer surface,which migration can adversely affect various desired properties such astriboelectrification of crosslinked organic porous particles designed tobe used as electrophotographic toners. The amount of the first andsecond pore stabilizing hydrocolloids used to prepare the first andsecond emulsions (and any additional emulsions) will depend on theamount of porosity and size of pores desired and the molecular weightand charge of the pore stabilizing hydrocolloid that is chosen. Forexample, the first and second pore stabilizing hydrocolloids can bedifferent in the first and second aqueous phases, resulting incrosslinked organic porous particles having first discrete pores thatare different in size from the second discrete pores. CMC isparticularly useful as a pore stabilizing hydrocolloid in both first andsecond water-in-oil emulsions in an amount of at least 0.5 weight % andup to and including 20 weight %, or at least 1 weight % and up to andincluding 10 weight %, based on the total weight of first and secondaqueous phases used in each emulsion. In some embodiments, theconcentrations of the first and second pore stabilizing hydrocolloidsare different in the first and second aqueous phases, resulting in acrosslinked organic porous particle having first discrete pores that aredifferent in size from the second discrete pores.

The first and second aqueous phases used in forming the first and secondwater-in-oil emulsions can additionally contain, if desired, salts tobuffer the emulsions and optionally to control the osmotic pressure ofthe aqueous phases. When CMC is used, for example, the osmotic pressurecan be increased by buffering using a pH 7 buffer. The first and secondemulsions can also contain additional pore forming agents such asammonium carbonate.

The first and second polyfunctional reactive compounds used in the firstand second oil phases (or additional oil phases) are crosslinkablethrough chain growth or step growth polymerization reactions. Themechanistic pathways in each of these reactions are different.Chain-growth polymerization proceeds as a result of free-radicals orions, whereas in step-growth polymerization, functional groups reactwith each other to increase the chain length or crosslink chains. Thisdistinction was introduced by Paul Flory in 1953, as described in“Principles of Polymer Chemistry”, Cornell University Press, 1953, p.39.

Polyfunctional reactive compounds suitable for chain growthpolymerization include polyfunctional polymerizable monomers andoligomers such as acrylate and methacrylate oligomers [the term“(meth)acrylate” used herein refers to acrylate and methacrylate] ofpolyfunctional compounds, such as polyhydric alcohols and theirderivatives having (meth)acrylate functional groups such as ethoxylatedtrimethylolpropane tri(meth)acrylate, tripropylene glycoldi(meth)acrylate, trimethylolpropane tri(meth)acrylate, diethyleneglycol di(meth)acrylate, pentaerythritol tetra(meth)acrylate,pentaerythritol tri(meth)acrylate, dipentaerythritol hexa(meth)acrylate,1,6-hexanediol di(meth)acrylate, or neopentyl glycol di(meth)acrylateand mixtures thereof, and acrylate and methacrylate oligomers derivedfrom low-molecular weight polyester resins, polyether resins, epoxyresins, polyurethane resins, alkyd resins, spiroacetal resins, epoxyacrylates, polybutadiene resins, and polythiol-polyene resins, andmixtures thereof that are capable of being dissolved in a suitablesolvent or diluent monomers (described below) that are immiscible withthe aqueous water phases and are substantially insoluble in water.

Additional polyfunctional reactive compounds suitable for chain growthpolymerization also include polyfunctional monomers such as divinylbenzene, ethylene glycol dimethacrylate, trimethylolpropane triacrylate,hexanediol dimethacrylate, tripropylene glycol dimethacrylate,diethylene glycol dimethacrylate, pentaerythritol triacrylate,dipentaerythritol hexamethacrylate, and neopentyl glycoldi(meth)acrylate, and mixtures thereof.

Useful polyfunctional reactive compounds suitable for chain growthpolymerization include urethane acrylate and methacrylate oligomers thatare derived from reacting diisocyanates with a oligo(poly)ester oroligo(poly)ether polyol to yield an isocyanate terminated urethane.Subsequently, hydroxy terminated acrylates are reacted with the terminalisocyanate groups. This acrylation provides unsaturation at the ends ofthe oligomer. The aliphatic or aromatic nature of the urethane acrylateis determined by the choice of diisocyanates. An aromatic diisocyanate,such as toluene diisocyanate, will yield an aromatic urethane acrylateoligomer. An aliphatic urethane acrylate will result from the selectionof an aliphatic diisocyanate, such as isophorone diisocyanate or hexylmethyl diisocyanate. Beyond the choice of isocyanate, the polyolbackbone plays a pivotal role in determining the performance of thefinal the oligomer. Polyols are generally classified as esters, ethers,or a combination of these two. The oligomer backbone is terminated bytwo or more acrylate or methacrylate units, which serve as reactivesites for chain growth polymerization. Choices among isocyanates,polyols, and acrylate or methacrylate termination units allowconsiderable latitude in the development of urethane acrylate oligomers.Urethane acrylates like most oligomers as polybutadiene acrylatecompounds are typically high in molecular weight and viscosity. Thesemultifunctional reactive compounds contain multiple reactive sites.Their functionality can vary from 2 to 6. Particularly usefulpolyfunctional reactive compounds for chain growth polymerizationinclude polyfunctional acrylic esters such as polybutadienedimethacrylate and 1,6-hexanediol diacrylate, and polyhydric alcoholsand their derivatives, such as mixtures of acrylate derivatives ofpentaerythritol including pentaerythritol tetraacrylate andpentaerythritol triacrylate functionalized aliphatic urethanes derivedfrom isophorone diisocyanate. Examples of useful urethane acrylateoligomers and polybutadiene dimethacrylate compounds are commerciallyavailable oligomers from Sartomer Company (Exton, Pa.), such as CN 968and CN301.

Polyfunctional reactive compounds suitable for step growthpolymerizations include polymers such as those derived from vinylmonomers and condensation monomers such as esters and mixtures thereof.Such polymers include those that have an acid or hydroxyl number greaterthan 2, but are not limited to polymers such as polyesters,polyurethanes, urethane acrylic copolymers, epoxy resins, siliconeresins, polyamide resins, modified rosins, paraffins, and waxes. Stillother useful polymers are polyesters of aromatic or aliphaticdicarboxylic acids with one or more aliphatic diols, such as polyestersof isophthalic or terephthalic or fumaric acid with diols such asethylene glycol, cyclohexane dimethanol, and bisphenol adducts ofethylene or propylene oxides. Such polymers can also be derived fromvinyl monomers such as styrenic polymers, monoolefin polymers (forexample, polymers formed from one or more of ethylene, propylene,butylene, and isoprene), vinyl ester polymers (for example, polymerformed from one or more of vinyl acetate, vinyl propionate, vinylbenzoate, and vinyl butyrate), polymers formed from one or moreα-methylene aliphatic monocarboxylic acid esters (for example, polymersformed from one or more of methyl acrylate, ethyl acrylate, butylacrylate, dodecyl acrylate, octyl acrylate, phenyl acrylate, methylmethacrylate, ethyl methacrylate, butyl methacrylate, and dodecylmethacrylate), vinyl ether polymers (such as polymers formed from one ormore of vinyl methyl ether, vinyl ethyl ether, and vinyl butyl ether),and vinyl ketone polymers (for example, polymers formed from one or moreof vinyl methyl ketone, vinyl hexyl ketone, and vinyl isopropenylketone), all of the above copolymerized with monomers such as(meth)acrylic acid, maleic acid, hydroxyethyl (meth)acrylate and thelike to result in polyfunctional reactive compounds such that they arecapable of being crosslinked with a reagent that causes crosslinking,being dissolved in a suitable solvent or ethylenically unsaturatedmonomers (described below) that are immiscible with the aqueous waterphases and are substantially insoluble in water.

Ethylenically unsaturated polymerizable monomers useful in thisinvention include monofunctional monomers, such as acrylate andmethacrylate monomers, and vinyl monomers, for example, methylmethacrylate, butyl acrylate, styrene, vinyl pyrrolidone, and mixturesthereof. It is not outside the scope of this invention to usemonoethylenically unsaturated oligomers in place of or in addition tothe ethylenically unsaturated monomers described above.

Polyfunctional reactive compounds, crosslinkable through chain growthpolymerization or step growth polymerization that can be used in any orall of the oil phases are described above.

When an oil phase contains one or more of the polyfunctional reactivecompounds that are crosslinkable through chain growth polymerizationreactions including ethylenically unsaturated polymerizable monomersdescribed above, that oil phase also includes a suitable reagent thatcauses crosslinking that is typically a free radical initiator thatprovides free radicals useful for initiating and continuing free radicalchain growth polymerization. Useful free radical initiators for chaingrowth polymerization reactions well known in the art and include suchclasses of compounds as azo compounds, peroxides, and other oil-solublefree radical initiators that are readily available from a number ofcommercial sources. A skilled worker would understand how much of aspecific free radical initiator would be best for specific monomers.Typically, a free radical initiator is present in an amount of at least1 weight % and up to and including 5 weight % based on the total weightof the polyfunctional reactive compound and the ethylenicallyunsaturated monomers that can be polymerized by chain growthpolymerization. The free radical initiator can be activated by heat orlight such as UV radiation. The temperature or wave length of light useddepends on the half life of the initiator at the desired temperature orthe absorption characteristics of the photoinitiator respectively.

When an oil phase contains one or more of the polyfunctional reactivecompounds crosslinkable through step growth polymerization reactionsmonomers described above, that oil phase also includes a suitablereagent that causes crosslinking that is typically a reactive compoundthat provides appropriate functional groups for step growthpolymerization. Useful step growth polymerization reactions arepolyfunctional aziridines or polyfunctional glycidyl compounds. Examplesof useful reagents that cause crosslinking through step growthpolymerization include but are not limited to, CX-100, a polyfunctionalaziridine from DSM Neo Resins, ERISYS GE240, a tetra glycidyl m-xylenediamine from CVC Thermoset Specialities, butanediol diglycidyl ether,2,3-dihydroxydioxane, chromium potassium sulfate, and zinc ammoniumcarbonate.

Some embodiments include a mixture of first and second crosslinkedorganic porous particles, each type of crosslinked organic porousparticle being prepared as described above. For example, in the mixtureof crosslinked organic porous particles, the first, second, third, andfourth marker materials can be all different. Alternatively, the firstand third marker materials are the same, and the second and fourthmarker materials are different from all other marker materials. Thismixture of crosslinked organic porous particles can be prepared andprovided in powder form or in an aqueous or organic solvent suspension.

Any suitable organic solvent that will dissolve the polyfunctionalreactive compound and the ethylenically unsaturated polymerizablemonomers and that is also immiscible with water can be used to preparethe first and second emulsions (or additional emulsions). Such organicsolvents include but are not limited to, methyl acetate, ethyl acetate,propyl acetate, chloromethane, dichloromethane, vinyl chloride,trichloromethane, carbon tetrachloride, ethylene chloride,trichloroethane, toluene, xylene, cyclohexanone, 2-nitropropane,dimethyl carbonate, and mixtures of two or more of these solvents. Ethylacetate and propyl acetate are generally good solvents for many usefulpolymers while being sparingly soluble in water, and they are readilyremoved as described below by evaporation. In the case where thepolyfunctional reactive compound is crosslinked using chain growthpolymerization, the organic solvent if used, is removed prior tocompletion of the crosslinking reaction. It can be removed after thewater-in-oil-in-water emulsion is formed and before the free radicalinitiator is activated by light or heat, or it can be removed after thechain growth polymerization is allowed to proceed partially or fully.The function of the solvent in all cases is not only to dissolve themultifunctional reactive compounds but also to provide a template forincreasing porosity by accommodating increased weight fraction of theaqueous phases in the first and second emulsions.

Optionally, the organic solvents that will dissolve the polymers andthat is immiscible with water can be a mixture of two or morewater-immiscible solvents chosen from the list given above.

The first and second oil can also contain emulsifiers to stabilize thefirst and second water-in-oil emulsions. Such emulsifiers usually have alow HLB number. Useful emulsifiers for the water-in-oil emulsionsinclude but are not limited to, sorbitan esters of fatty acids such asoleic acid and stearic acid, polyethylene oxide esters of fatty acids,Tetronic® 150R1 a tetrafunctional block copolymer with terminalsecondary hydroxyl groups (available from BASF Corporation), andpolyglycerol polyricinoleate, GRINDSTED® PGPR 90 (available fromDANISCO®).

Depending upon the ultimate use of the crosslinked organic porousparticles, the first and second emulsions can also include variousadditives, generally that are added to the polyfunctional reactivecompound and the ethylenically unsaturated polymerizable monomers priorto their dissolution in the organic solvent, during dissolution, orafter the dissolution step itself. Such additives can include but arenot limited to, colorants, charge control agents, shape control agents,compatibilizers, wetting agents, surfactants, plasticizers, and releaseagents such as waxes and lubricants, that are not within the pores asmarker materials. Combinations of these materials can also be used. Atleast one of the first and second aqueous phases can include a bufferingsalt, examples of which are readily known in the art.

The first and second emulsions (and any additional emulsions) used toprepare the crosslinked organic porous particles can be prepared by anyknown emulsifying technique and conditions using any type of mixing andshearing equipment. Such equipment includes but is not limited to, abatch mixer, planetary mixer, single or multiple screw extruder, dynamicor static mixer, colloid mill, high pressure homogenizer, sonicator, ora combination thereof. While any high shear type agitation device isuseful, a particularly useful homogenizing device is the Microfluidizer®such as Model No. 110T produced by Microfluidics Manufacturing operatingat >5000 psi (>351.5 kg_(f)/cm²). In this device, the droplets of thefirst and second aqueous phases can be dispersed separately and reducedin size in the respective oil (organic) phases in a high flow agitationzone and, upon exiting this zone, the particle size of the dispersedaqueous phases is reduced to uniform sized dispersed droplets in each ofthe oil phases. The temperature of the process can be modified toachieve the optimum viscosity for emulsification of the droplets and tominimize evaporation of the oil phases.

Optionally, the first and second water-in-oil emulsions can be combinedto form a third water-in-oil emulsion containing a mixture of the firstand second oil phases and distinct droplets of the first and secondaqueous phases. The first and second water-in-oil emulsions can becombined in any desirable weight ratio as long as at least one markermaterial is detectable. For example, in some embodiments, the weightratio of the first water-in-oil emulsion to the second oil-in-wateremulsion in the third water-in-oil emulsion can be from 1000:1 and toand including 0.01:1.

In some embodiments, a third oil phase (containing any of the organicsolvents from the list of organic solvents described above) containing athird polyfunctional reactive compound (chosen from the list ofpolyfunctional reactive compounds described above) or ethylenicallyunsaturated polymerizable monomers and a reagent that causescrosslinking initiators (as described above) can be combined with thefirst and second water-in-oil emulsions. The third polyfunctionalreactive compound can be the same or different from the first and secondpolyfunctional reactive compounds described above. The third oil phasecontaining the third polyfunctional reactive compound can be combined inthis manner in any suitable amount in relation to the first and secondwater-in-oil emulsions, for example, but not limited to, a weight ratioof at least 100:1 and to and including 1:100. The addition of the thirdoil phase allows the manufacturer to use stock solutions of the firstand second water-in-oil emulsions and to modify them as desired withouthaving to make up fresh water-in-oil emulsions.

Either the first water-in-oil or the third water-in-oil emulsion is thendispersed in a third aqueous phase that can contain a surfacestabilizing agent to form a water-in-oil-in-water emulsion containingdroplets of either the first water-in-oil emulsion or the thirdwater-in-oil emulsion, respectively. These third water-in-oil emulsiondroplets contain the distinct droplets of the first and second aqueousphases. The third water-in-oil emulsion can be dispersed within a thirdaqueous phase in the presence of a colloidal silica stabilizing agent toform a water-in-oil-in-water emulsion, containing an aqueous suspensionof oil droplets of the third water-in-oil emulsion, wherein the oildroplets contain discrete smaller droplets of the first aqueous phase,and second aqueous phase if present.

The resulting water-in-oil-in-water emulsion is subjected to shear orextensional mixing or similar flow processes, for example through acapillary orifice device to reduce the droplet size and achieve narrowsize distribution droplets through the limited coalescence process. ThepH of the third aqueous phase is generally between 4 and 7 whencolloidal silica is used as the stabilizing agent.

The suspension of droplets of the first water-in-oil (and secondwater-in-oil emulsion if present) in the third aqueous phase, results indroplets of polyfunctional reactive compound, or optionally anethylenically unsaturated polymerizable monomers and a reagent thatcauses crosslinking, dissolved in the oil containing the first aqueousphase (and second aqueous phase, if present) as distinct finer dropletswithin the bigger polymer droplets that upon solidification producediscrete porous domains in the resulting crosslinked organic porousparticles containing the polymer(s) as a crosslinked organic solidphase.

Useful surface stabilizing agents for the water-in-oil-in-wateremulsions include both water soluble polymers and small colloidalparticles, but are not limited to, stabilizer polymers such aspoly(vinyl pyrrolidone) and poly(vinyl alcohol), inorganic stabilizerssuch as clay particles, colloidal silica (for example LUDOX™ or NALCO™),or polymer latex particles as described in modified ELC processdescribed in U.S. Pat. No. 4,833,060 (Nair et al.), U.S. Pat. No.4,965,131 (Nair et al.), U.S. Pat. No. 2,934,530 (Ballast et al.), U.S.Pat. No. 3,615,972 (Morehouse et al.), U.S. Pat. No. 2,932,629 (Wiley),and U.S. Pat. No. 4,314,932 (Wakimoto et al.), the disclosures of whichare hereby incorporated by reference. Any combinations of these surfacestabilizing agents can also be used.

The actual amount of surface stabilizing agent used in the methoddepends on the size of the final crosslinked organic porous particlesdesired, which in turn depends upon the volume and weight ratios of thevarious phases used for making the multiple emulsions. While notintending to be limiting, the amount of surface stabilizing agent ineither or both emulsions can be at least 0.1 weight % and up to andincluding 30 weight %, or typically at least 0.1 weight % and up to andincluding 10 weight %, based on the total weight of thewater-in-oil-in-water emulsion and depending upon the surface activityof the stabilizer including, in the case of particulate stabilizers, theparticle size of the surface stabilizing agent (for example, colloidalor fumed silica particles). When such particulate stabilizers are used,the amount can be at least 0.2 weight % and up to and including 5 weight%.

Where the water-in-oil-in-water emulsion is formed, shear or extensionalmixing or flow process is controlled in order to minimize disruption ofthe distinct droplets of the first aqueous phase (and second aqueousphase, if present) in the oil phase(s). Droplet size reduction isachieved by homogenizing the final water-in-oil-in-water emulsionthrough a capillary orifice device, or other suitable flow geometry. Theshear field used to create the droplets in the finalwater-in-oil-in-water emulsion can be created using standard sheargeometries, such as an orifice plate or capillary. However, the flowfield can also be generated using alternative geometries, such as packedbeds of beads, or stacks or screens that impart an additionalextensional component to the flow. It is well known in the literaturethat membrane-based emulsifiers can be used to generate multipleemulsions. The techniques allow the droplet size to be tailored across awider range of sizes by adjusting the void volume or mesh size, and canbe applied across a wide range of flow rates. The back pressure suitablefor producing acceptable particle size and size distribution is at least100 psi and up to and including 5000 psi (7 kg_(f)/cm² to 351.5kg_(f)/cm²), or typically at least 500 psi and up to and including 3000psi (35.2 kg_(f)/cm² to 211 kg_(f)/cm²). The flow rate is generally atleast 1000 ml/min. and up to and including 6000 ml/min., particularlywhen a capillary orifice device is used.

The final size of the crosslinked organic porous particles and the finalsize of the pores of the crosslinked organic porous particles can beimpacted by the osmotic mismatch between the osmotic pressure of the oneor both of the first and second aqueous phases and the third aqueousphase. At each interface, the larger the osmotic pressure gradientpresent, the faster the diffusion rate where water will diffuse from thelower osmotic pressure phase to the higher osmotic pressure phasedepending on the solubility and diffusion coefficient in the oil(organic) phase. If the osmotic pressure of the third aqueous phase ishigher than the either or both of the first and second aqueous phases,then the water will migrate out of the pores of the crosslinked organicparticle and reduce the porosity and pore size. In order to maximizeporosity, one can tailor the osmotic pressures so that the osmoticpressure of the third aqueous phase is lower than the osmotic pressureof the first phase or both first and second aqueous phases. Thus, waterwill diffuse following the osmotic gradient from the third aqueous phaseinto the first aqueous phase (and second aqueous phase, if present)swelling the size of the distinct droplets of the first and secondaqueous phases thereby increasing the final porosity and pore size. Thisosmotic shock is desirably created after the homogenization of thewater-in-oil-in-water emulsion to minimize disruption of the distinctdroplets of the aqueous phases.

If it is desirable to have small pores and maintain the initial smalldrop size formed in the making of the first and second emulsions, theosmotic pressure of both the interior and exterior aqueous phase can bematched, or have only a small osmotic pressure gradient. Depending onthe osmotic pressure of each of the first and second aqueous phases andtheir values relative to the third aqueous phase, the resulting discretepores can have different average sizes.

Optionally, additional water can be added to the water-in-oil-in-wateremulsion before polymerization to increase the size of the pores bycreating an osmotic pressure mismatch between the first and secondaqueous phases as described above.

Once the water-in-oil-in-water emulsion has been formed, thepolyfunctional reactive compounds and optionally ethylenicallyunsaturated polymerizable monomer(s) supplied from one or both of thefirst and second water-in-oil emulsions, are polymerized to formprecursor crosslinked organic porous particles having a crosslinkedorganic solid phase including an external particle surface, and discretepores, and optionally first and second discrete pores that are isolatedfrom each other and dispersed within the crosslinked organic solidphase. This crosslinking can be instigated by the application of heat orpolymerizing radiation (for example actinic or IR or UV radiation) tothe water-in-oil-in-water emulsion as described earlier for initiatingcrosslinking by chain growth polymerization so that a polymerizationinitiator provides free radicals for monomer polymerization,crosslinking, and solidification. In the case of step growthpolymerization, generally crosslinking is instigated with heat usuallyduring solvent removal for solidification.

The first and second organic solvents, if present, are removed asdescribed earlier to produce an aqueous suspension of precursorcrosslinked organic porous particles containing discrete pores such asfirst and second pores that can contain suitable marker materials. Theprecursor crosslinked organic porous particles can then be subjected tosuitable isolation and drying techniques to provide the desiredcrosslinked organic porous particles, including removing water from thepores. The details of this process depend upon the type of thecrosslinking process, and the water solubility and boiling points of theorganic solvents in the oil phases relative to the temperature of thedrying process. Generally, however, organic solvents can be removed byevaporation using removal apparatus such as a rotary evaporator or aflash evaporator. The crosslinked organic porous particles can beisolated after removing the organic solvents by filtration orcentrifugation, followed by drying for example in an oven at 40° C. thatalso removes any water remaining in the pores. Optionally, thecrosslinked organic porous particles can be treated with alkali toremove any silica surface stabilizer particles.

The shape of the crosslinked organic porous particles can be modified ifnecessary for improved visualization of the marker materials usingmicroscopic techniques and to control the electrostatic toner transferand cleaning properties where such properties have been found to improveas the spherical nature (sphericity) of the crosslinked organic porousparticles is reduced (for example, an aspect ratio of less than 0.95, oran aspect ratio of from 0.4 and up to and including 0.95). Crosslinkedorganic porous particles that are not perfectly spherical can be usefulto improve the visualization of the marker materials in the pores. Thus,useful non-spherical crosslinked organic porous particles have an aspectratio of less than 0.95 and typically less than 0.9 and as low as 0.1.

In the method used to prepare the crosslinked organic porous particles,additives (shape control agents) can be incorporated into the first orsecond aqueous phases, in the first or second oil (organic) phase or inthe third aqueous phase to modify the shape, aspect ratio or morphologyof the crosslinked organic porous particles. The shape control agentscan be added after or prior to forming the water-in-oil-in-wateremulsion. In either case, the interfacial tension at the oil and thirdwater interface is modified before solvent is removed and crosslinkingreactions are completed, resulting in a reduction in sphericity of thecrosslinked organic porous particles. Some useful shape control agentsare quaternary ammonium tetraphenylborate salts described in U.S. PatentApplication Publication 2007/0298346 (Ezenyilimba et al.), metal saltsdescribed in U.S. Patent Application Publication 2008/0145780 (Yang etal.), carnauba waxes described in U.S. Pat. No. 5,283,151 (Santilli),SOLSPERSE® hyperdispersants as described in U.S. Pat. No. 5,968,702(Ezenyilimba et al.), metal salts as described in U.S. Pat. No.7,655,375 (Yang et al.), and zinc organic complexes as described in U.S.Pat. No. 7,662,535 (Yang et al.). All of these publications areincorporated herein by reference. The more desirable shape controlagents are polyethyloxazoline, fatty acid modified polyesters such asEFKA® 6225 and EFKA® 6220 from Ciba BASF, and phosphate esters ofalkoxylated phenols such as SynFac® 8337.

If the crosslinked organic porous particles are to be used as tonerparticles, they can also contain flow aids in the form of surfacetreatments that are typically in the form of inorganic oxides orpolymeric powders with typical particle sizes of at least 5 nm and up toand including 1000 nm. With respect to the surface treatment agent alsoknown as a spacing agent, the amount of the spacing agent on thecrosslinked organic porous particles is an amount sufficient to permitthe crosslinked porous toner particles to be stripped from carrierparticles in a two component dry developer by the electrostatic forcesassociated with the charged image or by mechanical forces. Usefulamounts of the spacing agent are at least 0.05% and up to and including10% or typically at least 0.1% and up to and including 5%, based on theweight of the crosslinked organic porous toner particle.

It should be understood from the description for providing crosslinkedorganic porous particles having first and second discrete pores, thatthe method for making these particles can be modified or expanded toincorporate additional discrete pores. To accomplish this, for example,the method described herein can further comprise:

combining one or more additional water-in-oil emulsions, each comprisinga pore stabilizing hydrocolloid in one or more additional aqueous phasesthat are dispersed in one or more additional oil phases each, and eachoil phase containing a polyfunctional reactive compound, a reagent thatcauses crosslinking, optionally an ethylenically unsaturatedpolymerizable monomer, and optionally a polymerization initiator,

with the first and second water-in-oil emulsions described above so thatthe third water-in-oil emulsion contains distinct droplets of the first,second, and the one or more additional aqueous phases.

In some embodiments of this method, at least one of the additionalwater-in-oil emulsions contains a marker material. Alternatively, atleast one additional water-in-oil emulsion contains no marker materials.In still other embodiments, at least one of the first or secondwater-in-oil emulsions contains multiple marker materials.

The crosslinked organic porous particles are insoluble in propyl acetatefor 24 hours at room temperature (from 20° C. to 25° C.) whereas thepolyfunctional reactive compounds used to make the crosslinked organicporous particles are generally soluble in propyl acetate under the sameconditions. In a particular embodiment, the crosslinking is achieved tosuch an extent that when the crosslinked organic porous particle issubjected to 200° C. and 1500 psi pressure (105.5 kg_(f)/cm²) for 5minutes, the crosslinked organic porous particle recovers at least 80%,and typically at least 95%, of its original volume (volume before beingsubjected to this test).

Articles and Methods of Labeling

The crosslinked organic porous particles can be incorporated intovarious articles. Such articles can be a fabric, label, film, fiber,paper sheet or plastic filmcard, paperstock, packaging component, orpolymer, ceramic, or glass article. In addition, the article cancomprise a coating composition (varnish or ink) comprising the one ormore crosslinked organic porous particles. The article can be a documenthaving the one or more crosslinked organic porous particles to provideauthenticity. Alternatively, the article is a formed polymer or glassarticle that comprises one or more crosslinked organic porous particles.

In such articles, the first and second marker materials can beindependently selected from the groups consisting of colored pigments orinks, fluorescing materials, radioisotopes, luminescing compounds,particles of metal or metal-containing compounds having a magneticmoment, and bioactive materials.

In some of the articles, the crosslinked organic porous particlesfurther comprise additional discrete pores besides the first and seconddiscrete pores. Such additional discrete pores can have no markermaterials.

The first and second discrete pores can comprise pore stabilizinghydrocolloids that are the same or different and are independentlyselected from the group consisting of carboxymethyl cellulose (CMC), agelatin or gelatin derivative, a protein or protein derivative, ahydrophilic synthetic polymer, a water-soluble microgel, a polystyrenesulfonate, poly(2-acrylamido-2-methylpropanesulfonate), and apolyphosphate.

The crosslinked organic porous particles can also be used in a method oflabeling an article with detectable information comprising:

incorporating one or more crosslinked organic porous particles into amaterial, or applying one or more crosslinked organic porous particlesto a substrate, each crosslinked organic porous particle comprising acrosslinked organic polymer that provides a crosslinked organic solidphase including an external particle surface and discrete pores that areisolated from each other and dispersed within the crosslinked organicsolid phase, the discrete pores having an average size greater than orequal to 0.1 μm, wherein the mode particle size of the porous particlesis at least 3 μm and up to and including 100 μm. In some embodiments,the crosslinked organic porous particles comprise first discrete porescomprising a first marker material, and second discrete pores comprisinga second marker material, which first and second marker materials aredetectably different.

In this method, the one or more crosslinked organic porous particles canbe applied to the substrate in a varnish or ink, or they can be appliedto the substrate in a paper or plastic label. Alternatively, the one ormore organic crosslinked organic porous particles can be introduced intothe material or applied to the substrate in a pattern. The substrate canbe a fiber or fabric.

A system of detection comprises:

a detectable composition comprising one or more crosslinked organicporous particles wherein each crosslinked organic porous particlecomprises a crosslinked organic polymer that provides a crosslinkedorganic solid phase including an external particle surface and discretepores that are isolated from each other and dispersed within thecrosslinked organic solid phase, the discrete pores having an averagesize greater than or equal to 0.1 μm, wherein the mode particle size ofthe crosslinked organic porous particles is at least 3 μm and up to andincluding 50 μm, and

an instrument for detecting one or both of the first and second markersin the crosslinked organic porous particles.

The present invention provides at least the following embodiments andcombinations thereof, but other combinations of features are consideredto be within the present invention as a skilled artisan would appreciatefrom the teaching of this disclosure:

1. A method for preparing a crosslinked organic porous particlecomprising:

providing a first water-in-oil emulsion comprising a first porestabilizing hydrocolloid in a first aqueous phase that is dispersed in afirst oil phase, which first oil phase comprises a first polyfunctionalreactive compound, a first reagent that causes crosslinking, optionallyat least one first ethylenically unsaturated polymerizable monomer, andoptionally a first organic solvent, and

optionally providing a second water-in-oil emulsion comprising a secondpore stabilizing hydrocolloid in a second aqueous phase that isdispersed in a second oil phase, which second oil phase comprises asecond polyfunctional reactive compound, a second reagent that causescrosslinking, optionally at least one ethylenically unsaturatedpolymerizable monomer, and optionally a second organic solvent,

optionally combining the first and second water-in-oil emulsions to forma third water-in-oil emulsion containing a mixture of the first andsecond oil phases and distinct droplets of the first and second aqueousphases,

dispersing either the first water-in-oil emulsion or the thirdwater-in-oil emulsion in a third aqueous phase containing a surfacestabilizing agent to form a water-in-oil-in-water emulsion containingdroplets of either the first water-in-oil emulsion or droplets of thethird water-in-oil emulsion, which third water-in-oil emulsion dropletscontain the distinct droplets of the first and second aqueous phases,and

polymerizing the polyfunctional reactive compounds and optionally theethylenically unsaturated polymerizable monomers to form a precursorcrosslinked organic porous particle having a crosslinked organic solidphase including an external particle surface, and discrete pores,optionally first and second discrete pores, being isolated from eachother and dispersed within the crosslinked organic solid phase,

removing, if present, the first and second organic solvents to producean aqueous suspension of the precursor crosslinked organic porousparticle, and

isolating the precursor crosslinked organic porous particle to provide acrosslinked organic porous particle.

2. The method of embodiment 1 wherein the first water-in-oil emulsionfurther comprises a first marker material that is incorporated into thefirst discrete pores, and wherein the second water-in-oil emulsionfurther comprises a second marker material that is incorporated into thesecond discrete pores.

3. The method of embodiment 2 wherein at least one of the first andsecond marker materials is selected from the group consisting of coloredpigments or dyes, fluorescing materials, radioisotopes, luminescingcompounds, particles of metal and metal-containing compounds havingmagnetic moments, luminescing compounds, and bioactive materials.

4. The method of any of embodiments 1 to 3 wherein the first and secondsurface stabilizing agents are independently a poly(vinyl pyrrolidone),poly(vinyl alcohol), clay particles, colloidal silica, fumed silica,polymer latex particles, or any combination thereof.

5. The method of any of embodiments 1 to 4 wherein the first and secondsurface stabilizing agents are independently present in an amount of atleast 0.1 weight % and up to an including 10 weight % of thewater-in-oil-in-water emulsion.

6. The method of any of embodiments 1 to 5 wherein each of the first andsecond surface stabilizing agents is colloidal or fumed silica that ispresent in an amount of at least 0.2 weight % and up to and including 5weight % of the water-in-oil-in-water emulsion.

7. The method of any of embodiments 1 to 6 wherein one or both of thefirst and second oil phases comprise a colorant, release agent, chargecontrol agent, shape control agent, compatibilizer, wetting agent,surfactant, plasticizer, wax, or lubricant, or any combination of thesematerials.

8. The method of any of embodiments 1 to 7 wherein at least one of thefirst and second aqueous phases comprises a buffering salt.

9. The method of any of embodiments 1 to 8 further comprising drying thecrosslinked organic porous particle.

10. The method of any of embodiments 1 to 9 wherein the first or secondoil phases comprises an organic solvent that is selected from the groupconsisting of ethyl acetate, propyl acetate, chloromethane,dichloromethane, vinyl chloride, trichloromethane, carbon tetrachloride,ethylene chloride, trichloroethane, toluene, xylene, cyclohexanone,dimethyl carbonate, and 2-nitropropane, and a mixture of two or more ofthese solvents.

11. The method of any of embodiments 1 to 10 wherein after forming thewater-in-oil-in-water emulsion and before polymerizing, adding water tothe water-in-oil-water emulsion.

12. The method of any of embodiments 1 to 11 wherein the weight ratio ofthe first water-in-oil emulsion to the second water-in-oil emulsioncombined in the third water-in-oil emulsion is from 1000:1 and up to andincluding 0.01:1.

13. The method of any of embodiments 1 to 12 comprising dispersing thethird water-in-oil emulsion in the third aqueous phase using a capillaryorifice device.

14. The method of embodiment 13 comprising dispersing the thirdwater-in-oil emulsion in the third aqueous phase using a back pressureof at least 100 psi (7 kg_(f)/cm²) and up to and including 5000 psi(351.5 kg_(f)/cm²) using a flow rate of at least 1000 ml/min. and up toand including 6000 ml/min.

15. The method of any of embodiments 1 to 14 further comprising:

combining one or more additional water-in-oil emulsions, each comprisinga pore stabilizing hydrocolloid in one or more additional aqueous phasesthat are dispersed in one or more additional oil phases each, and eachoil phase containing a polyfunctional reactive compound, a reagent thatcauses crosslinking, optionally an ethylenically unsaturatedpolymerizable monomer, and optionally an organic solvent,

with the first and second water-in-oil emulsions so that the thirdwater-in-oil emulsion contains distinct droplets of the first, second,and the one or more additional aqueous phases.

16. The method of embodiment 15 wherein at least one of additionalwater-in-oil emulsions contains a marker material.

17. The method of embodiment 15 or 16 further comprising at least oneadditional water-in-oil emulsion that contains no marker materials.

18. The method of any of embodiments 1 to 17 wherein the first andsecond pore stabilizing hydrocolloids are independently selected fromthe group consisting of carboxymethyl cellulose (CMC), a gelatin orgelatin derivative, a protein or protein derivative, a hydrophilicsynthetic polymer, a water-soluble microgel, a polystyrene sulfonate,poly(2-acrylamido-2-methylpropanesulfonate), a polyphosphate, andmixtures thereof.

19. The method of any of embodiments 1 to 18 wherein the first andsecond pore stabilizing hydrocolloids are different, resulting in acrosslinked organic porous particle having first discrete pores that aredifferent in size from the second discrete pores.

20. The method of any of embodiments 1 to 19 wherein the concentrationsof the first and second pore stabilizing hydrocolloids are different inthe first and second aqueous phases, resulting in a crosslinked organicporous particle having first discrete pores that are different in sizefrom the second discrete pores.

21. The method of any of embodiments 1 to 20 that provides a crosslinkedorganic porous particle having an aspect ratio of at least 0.95.

22. The method of any of embodiments 1 to 20 that provides a crosslinkedorganic porous particle having an aspect ratio of at least 0.1 and up toand including 0.95.

23. The method of any of embodiments 1 to 22 wherein at least one of thefirst and second oil phases contains a shape control agent.

24. The method of any of embodiments 1 to 23 wherein the third aqueousphase contains a shape control agent.

25. The method of any of embodiments 1 to 24 that provides a crosslinkedorganic porous particle having an aspect ratio of at least 0.4 and up toand including 0.95 by including a fatty acid modified polyester,polyethyloxazoline, or a phosphate ester of an alkoxylated phenol in thefirst, second, or third aqueous phase or in the first or second oilphase.

26. The method of any of embodiments 1 to 25 comprising polymerizing bythe application of heat or polymerization radiation to thewater-in-oil-in-water emulsion.

The following Examples are provided to illustrate the practice of thisinvention and are not meant to be limiting in any manner. In thefollowing Examples:

The polyester resins, Kao E and Kao E-B were obtained from KaoSpecialties Americas LLC, a part of Kao Corporation (Japan).

The monomers, styrene, methyl methacrylate, 2-ethylhexyl methacrylateand ethylene glycol dimethacrylate were obtained from Sigma Aldrich Co.

The prepolymers, CN968, an aliphatic urethane hexaacrylate oligomer andCN301, a mixture of polybutadiene dimethacrylate and 1,6-hexanedioldiacrylate esters, were obtained from Sartomer USA, LLC.

Carboxy methylcellulose, MW 250K (CMC), was obtained from Acros Organicsor from Ashland Aqualon as Aqualon 9M31F. These were interchangeablyused.

The emulsifiers, Tetronic® 150 R1, a tetrafunctional block copolymerwith terminal secondary hydroxyl groups, was obtained from BASFCorporation. Polyglyerol polyricinoleate, GRINDSTED® PGPR 90, wasobtained from DANISCO®.

Nalco™ 1060 colloidal silica was obtained from Nalco Chemical Company asa 50 weight % aqueous dispersion.

Ludox® TM colloidal silica was obtained from W.R Grace and Co. as a 50weight % aqueous dispersion.

EFKA 6225 and EFKA 6220, fatty acid modified polyesters, used as a shapecontrol agents were obtained from Ciba Specialty Chemicals. Thesecondary shape control agent, poly(2-ethyl-2-oxazoline), was obtainedfrom Aldrich.

The initiator, Vazo 52, 2,2′-azobis(2,4-dimethylvaleronitrile), wasobtained from DuPont Company.

A promoter, poly(methylamino ethanol adipate) oligomer (AMAE) that wasused to promote the adsorption of silica to droplet surface was preparedby condensation polymerization of amino ethanol and adipic acid.

Potassium dichromate was used to inhibit formation of water solublepolymer and was obtained from Aldrich.

The elastomeric material NOTIO™ was obtained from Mitsui ChemicalsAmerican, Inc.

The crosslinking agent CX100 is a polyfunctional aziridine that wasobtained from DSM NeoResins.

The marker materials used were cyan and magenta pigments. The cyan (C)pigment PB 15:3 (Sunfast Blue 15:3) was obtained from Sun Chemicals. Themagenta (M) pigment PR 122 (Toner Magenta E02) was obtained fromClariant. These pigments were milled in water using dispersants prior toincorporation in the first and second aqueous phases. The cyan“millgrind” (CM) was made using Solsperse® 43000 (30 weight % withrespect to pigment) as the dispersant at 18 weight % of pigment. Themagenta “millgrind” (MM) was made using Disperbyk® 190 (25 weight % withrespect to pigment) as the dispersant at 16 weight % of pigment.

One of the black marker materials used was a hydrophobic carbon black(CB) Toolkit C, obtained from Cabot Corporation. The CB mill grind (CBM)was made using Solsperse® 43000 (25 weight % with respect to CB) at 16weight % pigment. The other was a hydrophobic CB made in-house fromsurface modification of Regal 330 (Cabot Corporation), the mill grind ofwhich (CBM1) was made using Solsperse® 43000 (25 weight % with respectto CB) at 12 weight % pigment.

The size and shape of the porous particles were measured using a SysmexFPIA-3000 automated particle shape and size analyzer from MalvernInstruments. In this method, samples were passed through a sheath flowcell that transformed the particle suspension into narrow or flat flow,ensuring that the largest area of the particle is oriented towards thecamera and that all particles are in focus. The CCD camera captures 60images every second and these were analyzed in real time. Numericalevaluation of particle shape was derived from measurement of the area ofthe particle. A number of shape factors were calculated includingcircularity, aspect ratio, and circle equivalent diameter. Aspect ratio(AR) is defined as described above. The reported size of the particlesis the mode value of the particle size distribution where moderepresents the size that occurs most frequently.

The porosity of the porous particles was measured using mercuryintrusion porosimetry.

The crosslinked organic porous particles prepared according to thisinvention were evaluated using optical microscopy at both 600× and 1000×magnification for visualizing the marker materials in the discretepores. The test used for evaluating robustness of the crosslinkedorganic porous particles in a coating lacquer such as a UV curablecomposition, was suspending the particles in propyl acetate for 24 hoursor more followed by microscopic examination to look for particleintegrity. Propyl acetate was chosen since it is a good solvent for awide variety of non-crosslinked binders.

The crosslinked and non-crosslinked organic porous polymer particlesused in the Examples were made using the following procedures:

Control 1 Non-crosslinked Organic Porous Particle Containing 4 Weight %Cyan Marker Materials

A first organic phase (105 g) containing 75 weight % of methylmethacrylate, 25 g of styrene, 2 g of Tetronic 150R1, and 3.0 g of Vazo®52 was emulsified with the first aqueous phase containing 9.2 g of a 6.8weight % of CMC and 22.2 g of CM using the Silverson Mixer followed byhomogenization in the Microfluidizer® at 9800 psi (690 kg_(f)/cm²). An80 g aliquot of the water-in-oil emulsion was added to the third aqueousphase consisting of 111 g of a 200 mmolar citrate phosphate buffer at pH4, 7.1 g of Nalco 1060, and 0.9 g of a 10 weight % AMAE promoter inwater and was emulsified using the Silverson Mixer fitted with aGeneral-Purpose Disintegrating Head for two minutes at 2000 RPM,followed by homogenization in an orifice disperser at 1000 psi (70.4kg_(f)/cm²) to form a water-in-oil-in-water emulsion. This emulsion waspolymerized at 55° C. for 16 hours under nitrogen and then at 70° C. for4 hours. The resultant non-crosslinked organic porous particles wereisolated in a fitted glass funnel followed by washing with water anddrying. These non-crosslinked, cyan-colored porous particles had anominal particle size of 13.5 μm, an AR of 0.96, a porosity of 20%, anddistinct cyan pores. Some of the non-crosslinked organic porousparticles were added to propyl acetate and held for 24 hours. It wasobserved that these particles had swollen and began to dissolve in thepropyl acetate at the end of the time period.

Control 2 Non-crosslinked Organic Porous Particles (Containing 4 Weight% Cyan and Magenta Marker Materials

A first organic phase (289 g) containing 17 weight % of Kao E-B, inethyl acetate was emulsified using the Silverson Mixer followed byhomogenization in the Microfluidizer® at 9800 psi (690 kg_(f)/cm²) witha first aqueous phase prepared with 36.81 g of a 2.4 weight % of CMC and16 g of CM to give a first cyan water-in-oil emulsion. A secondwater-in-oil emulsion was prepared with 331 g of a second organic phaseconsisting of 17 weight % of Kao EB, in ethyl acetate and was emulsifiedwith a second aqueous phase containing 40.45 g of a 2.4 weight %solution of CMC and 20 g of MM in the same manner as the firstwater-in-oil emulsion. A 300 g aliquot of the first water-in-oilemulsion and a 300 g aliquot of the second water-in-oil emulsion werecombined with gentle mixing. This mixture of first and secondwater-in-oil emulsions was then added to a third aqueous phaseconsisting of 960 g of a 200 mmolar citrate phosphate buffer at pH 4 and19.7 g of Nalco 1060 and was emulsified using the Silverson Mixer fittedwith a General-Purpose Disintegrating Head for two minutes at 2000 RPM,followed by homogenization in an orifice disperser at 1000 psi (70.4kg_(f)/cm²) to form a water-in-oil-in-water emulsion. This emulsion wasthen diluted with an equal weight of water. The ethyl acetate wasevaporated using a Heidolph Laborata rotary evaporator at 40° C. underreduced pressure. The resulting suspension of beads was isolated in afitted glass funnel followed by washing with water and drying.

The purplish colored non-crosslinked organic porous particles had a modeparticle size of 14.6 μm, an AR of 0.98, and a porosity of 28%. They haddistinct cyan and magenta markers in separate discrete pores. Some ofthe non-crosslinked organic porous particles were added to propylacetate and held for 24 hours. It was observed that the particles hadswollen and began to dissolve in the propyl acetate at the end of thetime period.

Invention Example 1 Crosslinked Organic Porous Particles ContainingCarbon Black (7.5 weight %) in Discrete Pores

A first organic phase (190 g) containing 52.3 weight % of CN968, 42.4weight % of methyl methacrylate, 2.1 weight % of Tetronic® 150R1, and3.1 weight % of Vazo® 52 was emulsified with the first aqueous phasemade up of 89.7 g of CBM (containing of 2 weight % of CMC) using theSilverson Mixer followed by homogenization in the Microfluidizer® at9800 psi (689 kg_(f)/cm²). A 170 g aliquot of the first water-in-oilemulsion was added to the third aqueous phase consisting of 236 g of a200 mmolar citrate phosphate buffer at pH 4 and 16.5 g of Ludox® TM, andwas emulsified using the Silverson Mixer fitted with a General-PurposeDisintegrating Head for two minutes at 2000 RPM, followed byhomogenization in an orifice disperser at 1000 psi (70.3 kg_(f)/cm2) toform a water-in-oil-in-water emulsion. This emulsion was polymerized at55° C. for 16 hours under nitrogen and then at 70° C. for 4 hours. Theresulting spherical crosslinked organic porous particles were isolatedin a fitted glass funnel followed by washing with water and drying. Theblack-colored crosslinked organic porous particles had a mode particlesize of 8.2 μm and a porosity of 30% by Hg intrusion porosimetry. Thesedry particles were loaded into a flexible low density, transparentelastomer material NOTIO™, at 50 weight % by mixing in a Brabender at220 C and 15 rpm over a 10 minute period followed by another 5 minutesat 45 rpm. The sample was then pressed between 2 pieces of Kapton®polyimide film (DuPont) at 200° C. in a Carver Press for 5 minutes at3500 psi (246 kg_(f)/cm²) of pressure. Cross-sections of the crosslinkedorganic porous particle loaded elastomer showed that the crosslinkedorganic porous particles were intact and had not collapsed despite theirexposure to high pressure and temperature.

Invention Example 2 Crosslinked Organic Porous Particles Containing Cyanand Magenta Marker Materials (4 weight %) in Discrete Pores

A first organic phase (196 g) containing 52.3 weight % of CN968, 42.4weight % of methyl methacrylate, 2.1 weight % of Tetronic® 150R1, and3.1 weight % of Vazo® 52 was emulsified with the first aqueous phaseprepared with 17.5 g of a 10 weight % of CMC and 72.2 g of CM asdescribed in Invention Example 1. A second water-in-oil emulsion wasprepared with the second organic phase the same as the first organicphase, and the second aqueous phase containing 17.5 g of a 10 weight %solution of CMC and 72.2 g of MM in the same manner as the firstwater-in-oil emulsion. An 85 g aliquot of each of the first and secondwater-in-oil emulsions were mixed together gently and added to the thirdaqueous phase consisting of 118 g of a 200 mmolar citrate phosphatebuffer at pH 4, 4 g of Ludox® TM, and 3 g of 10 weight % AMAE promoterin water was emulsified, polymerized, and as isolated as described inInvention Example 1. The resulting purple-colored crosslinked organicporous particles had a mode particle size of 13.5 μm, an AR of 0.73, aporosity of 16%, and distinct cyan and magenta markers in discretepores. The crosslinked organic porous particles were added to propylacetate and held for 24 hours. The crosslinked organic porous particlesshowed no noticeable swelling or dissolution compared to thenon-crosslinked organic porous particles of Control 1 and the separatemarkers were distinctly visible.

The crosslinked organic porous particles of Invention Example 2 weredispersed as a dry powder in a commercial UV-curable lacquer using atouch-activated vibrating shaker for a couple of minutes. The resultingmixture was then coated onto a paper substrate using a Flexi Proofer,consisting of an Anilox roller (145 lines per inch, 368 lines per cm),doctor blade, and rubber transfer roller. After this coating onto thepaper substrate, the coating was passed through a Fusion UV SystemsP300MT at a speed of 100 feet/min. (3.048 m/min.) to harden the coating.

Using microscopy as described above, the coating was examined todetermine the ease of visual distinction of first and second markermaterials in discrete pores. In the coatings thus prepared for InventionExample 2, distinct domains of cyan and magenta marker materials couldbe seen.

Invention Example 3 Crosslinked Organic Porous Particles Containing Cyanand Magenta Marker Materials (3.9 weight %) in Discrete Pores

A first organic phase (196 g) containing 20 weight % of CN301, 59 weight% of methyl methacrylate, 1 weight % of EFKA 6220, 16 weight % of ethylacetate, 1.6 weight % of Tetronic® 150R1, and 2.4 weight % of Vazo® 52was emulsified with the first aqueous phase prepared with 1.3 g of 100weight % CMC in 11.65 g of water and 33.7 g of CM as described inInvention Example 1. A second water-in-oil emulsion was prepared withthe second organic phase the same as the first organic phase, and thesecond aqueous phase containing 47 g of a 1.9 weight % solution of CMCand 40 g of MM in the same manner as the first water-in-oil emulsion. An150 g aliquot of each of the first and second water-in-oil emulsionswere mixed together gently and added to the third aqueous phaseconsisting of 417 g of a 200 mmolar citrate phosphate buffer at pH 4,19.6 g of Nalco™ 1060, and 2.6 g of 10 weight % AMAE promoter in waterwas emulsified, polymerized, and isolated as described in InventionExample 1. The resulting purple-colored crosslinked organic porousparticles had a mode particle size of 15 μm, an AR of 0.94, a porosityof 21%, and distinct cyan and magenta markers in discrete pores. Thecrosslinked organic porous particles were added to propyl acetate andheld for 24 hours. The crosslinked organic porous particles showed nonoticeable swelling or dissolution compared to the non-crosslinkedorganic porous particles of Control 1 and the separate markers weredistinctly visible by microscopy.

Invention Example 4 Crosslinked Organic Porous Particles Containing Cyanand Magenta Marker Materials (4 weight %) in Discrete Pores

A first organic phase (98 g) containing 18 weight % of Kao E and 0.2weight % of EFKA 6225, in ethyl acetate was emulsified with a firstaqueous phase prepared with 23.8 g of a 2.5 weight % of CMC and 8.4 g ofCM as described in Invention Example 1 to give a first cyan water-in-oilemulsion. A second water-in-oil emulsion was prepared with 98 g of asecond organic phase consisting of 18 weight % of Kao E and 0.2 weight %of EFKA 6225 in ethyl acetate was emulsified with a second aqueous phasecontaining 24.1 g of a 2.5 weight % solution of CMC and 8 g of MM in thesame manner as the first water-in-oil emulsion. A 25 g aliquot of thefirst water-in-oil emulsion and a 25 g aliquot of the secondwater-in-oil emulsion were then added to 50 g of a 13.7 weight %solution of Kao E containing 0.07 g of EFKA 6225 in ethyl acetate and0.25 g CX100 with gentle mixing. This mixture of first and secondwater-in-oil emulsions was then added to a third aqueous phaseconsisting of 162 g of a 200 mmolar citrate phosphate buffer at pH 4 and5 g of Nalco™ 1060 and emulsified as described in Invention Example 1,to form a water-in-oil-in-water emulsion. This emulsion was then dilutedwith an equal weight of water containing a 0.03 weight % solution ofPEOX. The ethyl acetate was evaporated using a Heidolph Laborata rotaryevaporator at 40° C. under reduced pressure for 30 minutes followed by45C for 45 minutes to complete the crosslinking reaction of CX100. Theresulting purplish-colored crosslinked organic porous particles wereisolated as described in Invention Example 1 and had a mode particlesize of 15.4 μm, an AR of 0.80, and a porosity of 40%. They had distinctcyan and magenta markers in separate discrete pores. The crosslinkedorganic porous particles were added to propyl acetate and held for 24hours. They showed a little swelling but no dissolution compared to thenon-crosslinked organic porous particles of Control 2.

Invention Example 5 Crosslinked Organic Porous Particles Containing aCyan Marker Material (4 weight %) in Discrete Pores

Crosslinked organic porous particles were prepared the same as forControl 1 except that the first organic phase contained 75 g methylmethacrylate, 15 g styrene, and 10 g of ethylene glycol dimethacrylate.The resulting cyan-colored crosslinked organic porous particles had amode particle size of 13.2 μm, an AR of 0.971, a porosity of 25%, anddistinct cyan pores. They were added to propyl acetate and held for 24hours. The crosslinked organic porous particles showed no swelling ordissolution compared to the non-crosslinked organic porous particles ofControl 1.

Invention Example 6 Crosslinked Organic Porous Particles ContainingCarbon Black (10 weight %) in Discrete Pores

A first organic phase (243.7 g) containing 81 weight % ethyl acetate, 9weight % of CN301, 9 weight % of 2-ethylhexyl methacrylate, 0.4 weight %of PGPR 90, and 0.6 weight % of Vazo® 52 was emulsified with the firstaqueous phase made up of 80 grams of a 3.75 weight % CMC and 82.5 g ofCBM 1 using the Silverson Mixer followed by homogenization in theMicrofluidizer® at 9800 psi (689 kg_(f)/cm²). A 250 g aliquot of thefirst water-in-oil emulsion was added to the third aqueous phaseconsisting of 400 g of a 200 mmolar citrate phosphate buffer at pH 4, 16g of Nalco® 1060 and 2 g of a 10 weight % AMAE promoter solution inwater, and emulsified using the Silverson Mixer fitted with aGeneral-Purpose Disintegrating Head for two minutes at 2000 RPM,followed by homogenization in an orifice disperser at 1000 psi (70.3kg_(f)/cm²) to form a water-in-oil-in-water emulsion. This emulsion wasdiluted 1:1 with water followed by addition of 3 ml of a 2.5 weight %potassium dichromate to scavenge water soluble free radicals andpolymerized at 55° C. for 1 hour under nitrogen. This was followed byremoval of ethyl acetate under reduced pressure using a rotaryevaporator as in Example 4. The polymerization was then continued at 55°C. for 16 hours under nitrogen and then at 70° C. for 4 hours. Theresulting spherical crosslinked organic porous particles were isolatedin a fritted glass funnel followed by washing with water and drying. Theblack-colored crosslinked organic porous particles had a mode particlesize of 6.8 μm, an AR of 0.965, and a porosity of 50%. These dryparticles were added to propyl acetate and held for 24 hours. Thecrosslinked organic porous particles showed no swelling or dissolutionafter that time period. These dry particles were also loaded into aflexible low density, transparent elastomer material NOTIO™ at 50 weight% by mixing in a Brabender at 220° C. and 15 rpm over a 10 minute periodfollowed by another 5 minutes at 45 rpm. The sample was then pressedbetween 2 pieces of Kapton® polyimide film (DuPont) at 200° C. in aCarver Press for 5 minutes at 3500 psi (246 kg_(f)/cm²) of pressure.Cross-sections of the particle loaded elastomer showed that thecrosslinked organic porous particles were intact and had not collapseddespite their exposure to high pressure and temperature.

The invention has been described in detail with particular reference tocertain preferred embodiments thereof, but it will be understood thatvariations and modifications can be effected within the spirit and scopeof the invention.

1. A method for preparing a crosslinked organic porous particlecomprising: providing a first water-in-oil emulsion comprising a firstpore stabilizing hydrocolloid in a first aqueous phase that is dispersedin a first oil phase, which first oil phase comprises a firstpolyfunctional reactive compound, a first reagent that causescrosslinking, optionally at least one first ethylenically unsaturatedpolymerizable monomer, and optionally a first organic solvent, andoptionally providing a second water-in-oil emulsion comprising a secondpore stabilizing hydrocolloid in a second aqueous phase that isdispersed in a second oil phase, which second oil phase comprises asecond polyfunctional reactive compound, a second reagent that causescrosslinking, optionally at least one ethylenically unsaturatedpolymerizable monomer, and optionally a second organic solvent,optionally combining the first and second water-in-oil emulsions to forma third water-in-oil emulsion containing a mixture of the first andsecond oil phases and distinct droplets of the first and second aqueousphases, dispersing either the first water-in-oil emulsion or the thirdwater-in-oil emulsion in a third aqueous phase containing a surfacestabilizing agent to form a water-in-oil-in-water emulsion containingdroplets of either the first water-in-oil emulsion or droplets of thethird water-in-oil emulsion, which third water-in-oil emulsion dropletscontain the distinct droplets of the first and second aqueous phases,and polymerizing the polyfunctional reactive compounds and optionallythe ethylenically unsaturated polymerizable monomers to form a precursorcrosslinked organic porous particle having a crosslinked organic solidphase including an external particle surface, and discrete pores,optionally first and second discrete pores, being isolated from eachother and dispersed within the crosslinked organic solid phase,removing, if present, the first and second organic solvents to producean aqueous suspension of the precursor crosslinked organic porousparticle, and isolating the precursor crosslinked organic porousparticle to provide a crosslinked organic porous particle.
 2. The methodof claim 1 wherein the first water-in-oil emulsion further comprises afirst marker material that is incorporated into the first discretepores, and wherein the second water-in-oil emulsion further comprises asecond marker material that is incorporated into the second discretepores.
 3. The method of claim 2 wherein at least one of the first andsecond marker materials is selected from the group consisting of coloredpigments or dyes, fluorescing materials, radioisotopes, luminescingcompounds, particles of metal and metal-containing compounds havingmagnetic moments, luminescing compounds, and bioactive materials.
 4. Themethod of claim 1 wherein the first and second surface stabilizingagents are independently a poly(vinyl pyrrolidone), poly(vinyl alcohol),colloidal silica, fumed silica, clay particles, polymer latex particles,or any combination thereof.
 5. The method of claim 1 wherein the firstand second surface stabilizing agents are independently present in anamount of at least 0.1 weight % and up to an including 10 weight % ofthe water-in-oil-in-water emulsion.
 6. The method of claim 1 whereineach of the first and second surface stabilizing agents is colloidal orfumed silica that is present in an amount of at least 0.2 weight % andup to and including 5 weight % of the water-in-oil-in-water emulsion. 7.The method of claim 1 wherein one or both of the first and second oilphases comprise a colorant, release agent, charge control agent, shapecontrol agent, compatibilizer, wetting agent, surfactant, plasticizer,wax, or lubricant, or any combination of these materials.
 8. The methodof claim 1 wherein at least one of the first and second aqueous phasescomprises a buffering salt.
 9. The method of claim 1 further comprisingdrying the crosslinked organic porous particle.
 10. The method of claim1 wherein the first or second oil phases comprises an organic solventthat is selected from the group consisting of ethyl acetate, propylacetate, chloromethane, dichloromethane, vinyl chloride,trichloromethane, carbon tetrachloride, ethylene chloride,trichloroethane, toluene, xylene, cyclohexanone, dimethyl carbonate, and2-nitropropane, and a mixture of two or more of these solvents.
 11. Themethod of claim 1 wherein after forming the water-in-oil-in-wateremulsion and before polymerizing, adding water to the water-in-oil-wateremulsion.
 12. The method of claim 1 wherein the weight ratio of thefirst water-in-oil emulsion to the second water-in-oil emulsion combinedin the third water-in-oil emulsion is from 1000:1 and up to andincluding 0.01:1.
 13. The method of claim 1 comprising dispersing thethird water-in-oil emulsion in the third aqueous phase using a capillaryorifice device.
 14. The method of claim 13 comprising dispersing thethird water-in-oil emulsion in the third aqueous phase using a backpressure of at least 100 psi (7 kg_(f)/cm²) and up to and including 5000psi (351.5 kg_(f)/cm²) using a flow rate of at least 1000 ml/min. and upto and including 6000 ml/min.
 15. The method of claim 1 furthercomprising: combining one or more additional water-in-oil emulsions,each comprising a pore stabilizing hydrocolloid in one or moreadditional aqueous phases that are dispersed in one or more additionaloil phases each, and each oil phase containing a polyfunctional reactivecompound, a reagent that causes crosslinking, optionally anethylenically unsaturated polymerizable monomer, and optionally anorganic solvent, with the first and second water-in-oil emulsions sothat the third water-in-oil emulsion contains distinct droplets of thefirst, second, and the one or more additional aqueous phases.
 16. Themethod of claim 15 wherein at least one of additional water-in-oilemulsions contains a marker material.
 17. The method of claim 15 furthercomprising at least one additional water-in-oil emulsion that containsno marker materials.
 18. The method of claim 1 wherein the first andsecond pore stabilizing hydrocolloids are independently selected fromthe group consisting of carboxymethyl cellulose (CMC), a gelatin orgelatin derivative, a protein or protein derivative, a hydrophilicsynthetic polymer, a water-soluble microgel, a polystyrene sulfonate,poly(2-acrylamido-2-methylpropanesulfonate), a polyphosphate, andmixtures thereof.
 19. The method of claim 1 wherein the first and secondpore stabilizing hydrocolloids are different, resulting in a crosslinkedorganic porous particle having first discrete pores that are differentin size from the second discrete pores.
 20. The method of claim 1wherein the concentrations of the first and second pore stabilizinghydrocolloids are different in the first and second aqueous phases,resulting in a crosslinked organic porous particle having first discretepores that are different in size from the second discrete pores.
 21. Themethod of claim 1 that provides a crosslinked organic porous particlehaving an aspect ratio of at least 0.95.
 22. The method of claim 1 thatprovides a crosslinked organic porous particle having an aspect ratio ofat least 0.1 and up to and including 0.95.
 23. The method of claim 1wherein at least one of the first and second oil phases contains a shapecontrol agent.
 24. The method of claim 1 wherein the third aqueous phasecontains a shape control agent.
 25. The method of claim 1 that providesa crosslinked organic porous particle having an aspect ratio of at least0.4 and up to and including 0.95 by including a fatty acid modifiedpolyester, polyethyloxazoline, or a phosphate ester of an alkoxylatedphenol in the first, second, or third aqueous phase or in the first orsecond oil phase.
 26. The method of claim 1 comprising polymerizing bythe application of heat or polymerization radiation to thewater-in-oil-in-water emulsion.